TWI441691B - Device for characterisation of the granulometry of powders and its uses - Google Patents
Device for characterisation of the granulometry of powders and its uses Download PDFInfo
- Publication number
- TWI441691B TWI441691B TW096133694A TW96133694A TWI441691B TW I441691 B TWI441691 B TW I441691B TW 096133694 A TW096133694 A TW 096133694A TW 96133694 A TW96133694 A TW 96133694A TW I441691 B TWI441691 B TW I441691B
- Authority
- TW
- Taiwan
- Prior art keywords
- powder
- particle size
- characterizing
- size measurement
- powder according
- Prior art date
Links
- 239000000843 powder Substances 0.000 title claims description 233
- 238000012512 characterization method Methods 0.000 title 1
- 238000001033 granulometry Methods 0.000 title 1
- 230000007246 mechanism Effects 0.000 claims description 132
- 239000002245 particle Substances 0.000 claims description 130
- 238000005259 measurement Methods 0.000 claims description 92
- 238000012216 screening Methods 0.000 claims description 49
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 37
- 238000000034 method Methods 0.000 claims description 32
- 239000000463 material Substances 0.000 claims description 29
- 238000004519 manufacturing process Methods 0.000 claims description 28
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 24
- 239000011707 mineral Substances 0.000 claims description 24
- 238000005303 weighing Methods 0.000 claims description 17
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 16
- 238000004140 cleaning Methods 0.000 claims description 15
- 235000000346 sugar Nutrition 0.000 claims description 13
- 230000008878 coupling Effects 0.000 claims description 12
- 238000010168 coupling process Methods 0.000 claims description 12
- 238000005859 coupling reaction Methods 0.000 claims description 12
- 239000000919 ceramic Substances 0.000 claims description 8
- 235000013305 food Nutrition 0.000 claims description 8
- 239000004033 plastic Substances 0.000 claims description 8
- 229920003023 plastic Polymers 0.000 claims description 8
- -1 chalk Substances 0.000 claims description 7
- 239000013078 crystal Substances 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 239000003973 paint Substances 0.000 claims description 5
- 235000019738 Limestone Nutrition 0.000 claims description 4
- 239000010459 dolomite Substances 0.000 claims description 4
- 229910000514 dolomite Inorganic materials 0.000 claims description 4
- 239000003337 fertilizer Substances 0.000 claims description 4
- 235000013312 flour Nutrition 0.000 claims description 4
- 239000006028 limestone Substances 0.000 claims description 4
- 239000004579 marble Substances 0.000 claims description 4
- 235000013336 milk Nutrition 0.000 claims description 4
- 239000008267 milk Substances 0.000 claims description 4
- 210000004080 milk Anatomy 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- 238000007639 printing Methods 0.000 claims description 4
- 150000003839 salts Chemical class 0.000 claims description 4
- 244000043261 Hevea brasiliensis Species 0.000 claims description 3
- 239000003599 detergent Substances 0.000 claims description 3
- 229920001971 elastomer Polymers 0.000 claims description 3
- 239000000806 elastomer Substances 0.000 claims description 3
- 229920003052 natural elastomer Polymers 0.000 claims description 3
- 229920001194 natural rubber Polymers 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000000454 talc Substances 0.000 claims description 3
- 229910052623 talc Inorganic materials 0.000 claims description 3
- 239000011159 matrix material Substances 0.000 claims 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims 1
- 239000003814 drug Substances 0.000 claims 1
- 229940079593 drug Drugs 0.000 claims 1
- 238000004458 analytical method Methods 0.000 description 14
- 238000009826 distribution Methods 0.000 description 13
- 239000000523 sample Substances 0.000 description 11
- 238000012360 testing method Methods 0.000 description 9
- 238000005516 engineering process Methods 0.000 description 7
- 230000008901 benefit Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 230000006870 function Effects 0.000 description 6
- 230000003287 optical effect Effects 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 4
- 238000012417 linear regression Methods 0.000 description 4
- 238000005406 washing Methods 0.000 description 4
- 238000000576 coating method Methods 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 150000008163 sugars Chemical class 0.000 description 3
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 238000002425 crystallisation Methods 0.000 description 2
- 230000008025 crystallization Effects 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000001476 alcoholic effect Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000012620 biological material Substances 0.000 description 1
- 239000007767 bonding agent Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000001066 destructive effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000007907 direct compression Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000021550 forms of sugar Nutrition 0.000 description 1
- ZZUFCTLCJUWOSV-UHFFFAOYSA-N furosemide Chemical compound C1=C(Cl)C(S(=O)(=O)N)=CC(C(O)=O)=C1NCC1=CC=CO1 ZZUFCTLCJUWOSV-UHFFFAOYSA-N 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229910052588 hydroxylapatite Inorganic materials 0.000 description 1
- 238000010191 image analysis Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011005 laboratory method Methods 0.000 description 1
- 238000010309 melting process Methods 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 229910052753 mercury Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000010951 particle size reduction Methods 0.000 description 1
- 239000011236 particulate material Substances 0.000 description 1
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 description 1
- 230000008447 perception Effects 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000007619 statistical method Methods 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 description 1
Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
- G01N15/02—Investigating particle size or size distribution
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/18—Drum screens
- B07B1/22—Revolving drums
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B1/00—Sieving, screening, sifting, or sorting solid materials using networks, gratings, grids, or the like
- B07B1/18—Drum screens
- B07B1/22—Revolving drums
- B07B1/26—Revolving drums with additional axial or radial movement of the drum
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N15/00—Investigating characteristics of particles; Investigating permeability, pore-volume or surface-area of porous materials
- G01N2015/0096—Investigating consistence of powders, dustability, dustiness
Landscapes
- Chemical & Material Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Health & Medical Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- Physics & Mathematics (AREA)
- Dispersion Chemistry (AREA)
- General Health & Medical Sciences (AREA)
- Pathology (AREA)
- Combined Means For Separation Of Solids (AREA)
- Analysing Materials By The Use Of Radiation (AREA)
- Cosmetics (AREA)
- Sampling And Sample Adjustment (AREA)
- Glanulating (AREA)
Description
本發明有關裝置及設備之允許決定粉末的粒度測量之區段,在此尤其能夠線上地、亦即在該等粉末的製造過程之進展中進行該特徵記述。The section of the device and the device according to the invention which allows the determination of the particle size of the powder, in particular, can be carried out on the line, that is to say in the progression of the manufacturing process of the powders.
該等有關之粉末更特別地是乾燥粉末,亦即具有低於5質量百分比之水含量的粉末,如藉由該等粉末之乾燥前後的差別稱重之測量所決定。Such related powders are more particularly dry powders, i.e., powders having a water content of less than 5 mass percent, as determined by differential weighing measurements before and after drying of the powders.
該等有關之粉末係亦具有一寬廣之粒度測量範圍的粉末,亦即該粉末之平均直徑係於0.05及10毫米之間。The related powders also have a broad particle size measurement range, i.e., the powder has an average diameter between 0.05 and 10 mm.
該等有關之粉末係甚至在該食物生產方面中所使用之更特別的粉末,諸如以糖結晶為基礎之粉末、鹽粉、麵粉、奶粉、由脫水食品材料所構成之粉末、洗衣粉、陶瓷粉末、塑膠粉末、金屬粉末、油漆粉末、藥物粉末、用於印刷之碳粉、肥料、或再次由礦物物質所組成之粉末、與甚至更特別地是天然及/或沉澱之以碳酸鈣為基礎及/或以白雲石為基礎及/或以滑石為基礎之礦物物質粉末、且甚至更特別地是具有一以天然碳酸鈣為基礎之礦物物質的粉末,該礦物物質係大理石、白堊、石灰岩、或其混合物。These related powders are even more special powders used in the production of such foods, such as powders based on sugar crystals, salt powder, flour, milk powder, powders composed of dehydrated food materials, washing powder, ceramics. Powder, plastic powder, metal powder, paint powder, pharmaceutical powder, toner for printing, fertilizer, or powder composed of mineral matter again, and even more particularly natural and/or precipitated based on calcium carbonate And/or a mineral powder based on dolomite and/or based on talc, and even more particularly a powder having a mineral material based on natural calcium carbonate, which is marble, chalk, limestone, Or a mixture thereof.
本發明之第一目的係一用於粉末之粒度測量的特徵之裝置,該裝置設有一進給機構、一排空機構、一稱重機構、一連續震動機構、一篩選機構、及可能一控制機構,且其特徵為:-其中該篩選機構係一繞著水平軸心轉動之機構,具有用於一未被佔用的空間或一用於粉末之釋放及導入的空間之至少1位置、用於一抗衝擊板件之1位置、用於不同篩孔之2篩網的至少2位置;-及其中該裝置具有一清潔機構,該清潔機構由至少一噴嘴及/或一位在該篩選機構的周邊上之超音波發生器所組成;-及其中該裝置具有一彈性耦接機構,其位在該篩選機構的水平軸心與該連續震動機構之間。The first object of the present invention is a device for controlling the particle size of a powder, the device being provided with a feeding mechanism, an emptying mechanism, a weighing mechanism, a continuous vibration mechanism, a screening mechanism, and possibly a control a mechanism, and characterized in that: - wherein the screening mechanism is a mechanism that rotates about a horizontal axis, having at least one position for an unoccupied space or a space for release and introduction of powder, for 1 position of an impact resistant plate member, at least 2 positions of 2 screens for different mesh openings; and wherein the device has a cleaning mechanism consisting of at least one nozzle and/or one at the screening mechanism An ultrasonic generator on the periphery; and the device has an elastic coupling mechanism between the horizontal axis of the screening mechanism and the continuous vibration mechanism.
本發明之另一目的係為粉末之粒度測量的特徵、且尤其是其線上、亦即其製程的進展中之特徵使用此一裝置。Another object of the invention is to use such a device for the characteristics of the particle size measurement of the powder, and in particular for its on-line, i.e., the progress of its process.
這尤其有關乾燥粉末、亦即具有低於5質量百分比之水含量的粉末,如藉由該等粉末之乾燥前後的差別稱重之測量所決定。This relates in particular to dry powders, i.e. powders having a water content of less than 5 mass percent, as determined by the measurement of differential weighing before and after drying of the powders.
其亦有關具有一寬廣之粒度測量範圍的粉末,亦即該粉末之平均直徑係於0.05及10毫米之間。It is also related to powders having a broad particle size measurement range, i.e., the average diameter of the powder is between 0.05 and 10 mm.
最後,其有關在該食物生產方面中所使用之粉末,諸如以糖結晶為基礎之粉末、鹽粉、麵粉、奶粉、由脫水食品材料所構成之粉末、洗衣粉、陶瓷粉末、塑膠粉末、金屬粉末、油漆粉末、藥物粉末、用於印刷之碳粉、肥料、或再次由礦物物質所組成之粉末、與甚至更特別地是天然及/或沉澱之以碳酸鈣為基礎及/或以白雲石為基礎之礦物物質粉末、且甚至更特別地是具有一以天然碳酸鈣為基礎之礦物物質的粉末,該礦物物質係大理石、白堊、石灰岩、或其混合物。Finally, it relates to powders used in the production of foods, such as powders based on sugar crystals, salt powder, flour, milk powder, powders composed of dehydrated food materials, washing powder, ceramic powder, plastic powder, metal Powder, paint powder, pharmaceutical powder, toner for printing, fertilizer, or powder composed of mineral matter again, and even more particularly natural and/or precipitated based on calcium carbonate and/or dolomite A mineral-based powder, and even more particularly a powder having a mineral material based on natural calcium carbonate, which is marble, chalk, limestone, or a mixture thereof.
本發明之第一目的係一能夠使各種粉末之盡可能線上地粒度測量的特徵記述成為可能之裝置,該等粉末尤其諸如乾燥粉末,如上面所界定者,並具有一寬廣之粒度測量,亦如上面所界定,及尤其不同類別之粉末,如在該先前章節中所界定者。A first object of the present invention is a device capable of characterizing the particle size measurement of various powders as much as possible, such as a dry powder, as defined above, and having a broad particle size measurement, As defined above, and especially for different classes of powders, as defined in this prior section.
藉著該粒度測量之線上特徵記述,當這有關由礦物物質所組成之粉末時,該申請人意指於該等粉末之製造過程期間、及尤其於該粉末之粒度測量減少的過程期間之粒度測量的控制。By means of the on-line characteristic of the particle size measurement, when referring to a powder consisting of mineral materials, the applicant means particle size measurement during the manufacturing process of the powders, and especially during the process of reducing the particle size measurement of the powder. control.
本發明之另一目的係提供一能夠在一用於該等上述粉末之操作中記述不同粒度測量類別的特徵之裝置。Another object of the present invention is to provide an apparatus capable of characterizing different particle size measurement categories in the operation of such powders.
本發明之另一目的產生以下事實,即以此方式所製成之裝置在該等粉末的製造場所中之使用係簡單的,並與此一場所之工業限制條件相容的。Another object of the present invention is to produce the fact that the device made in this manner is simple to use in the manufacture of such powders and is compatible with the industrial constraints of the site.
本發明之另一目的係提供一能夠使該等粉末於其製造過程期間之粒度測量的特徵記述成為可能之裝置,而不會改變該等粉末或損壞該裝置:該微粒材料之用於分析的完整性係藉著此機制所維持,且維持該裝置隨著時間之消逝的使用壽命。Another object of the present invention is to provide a device capable of enabling the character description of the particle size measurement during the manufacturing process without altering the powder or damaging the device: the particulate material for analysis Integrity is maintained by this mechanism and maintains the life of the device over time.
本發明之另一目的係提供該裝置之自動清洗作用(而沒有在一操作員方面之操縱),既促成減少該維修成本,又促成維持該裝置之完整性及其結果之完整性。Another object of the present invention is to provide automatic cleaning of the device (without operator manipulation), both to reduce the cost of maintenance and to maintain the integrity of the device and the integrity of its results.
本發明之一最後目的係提供一允許記述該等粉末之粒度測量的特徵之裝置,在此該稱重系統不會被源自該連續震動機構之震動所損壞。A final object of the present invention is to provide a device that allows for the description of the characteristics of the particle size measurement of such powders, where the weighing system is not damaged by vibrations originating from the continuous vibrating mechanism.
應注意的是本發明必定實現這些最後的三個目標(該等粉末及裝置之保存、自動清洗、震動之消除),其中有助於實現這些目標之特徵係強制性的及非選擇性的。與法國專利第0504917號作比較,這是一基本差異。It should be noted that the present invention must achieve these last three objectives (preservation of such powders and devices, automatic cleaning, elimination of vibrations), wherein the features that contribute to achieving these objectives are mandatory and non-selective. This is a fundamental difference compared to French Patent No. 0504917.
於粉末之領域中,粒度測量之控制對於熟諳此技藝者、一通曉數門知識之工業製程工程師、一專門從事於有關粉狀材料之技術者係一基本要素。實際上,就礦物物質粉末之情況而言,此控制能夠使他了解在粒度測量減少之不同階段的進程中所製成之產品的品質。於乾燥粉末之更一般性領域中,及尤其是礦物物質粉末、塑膠粉末、金屬粉末、陶瓷粉末、或洗衣粉、與糖之領域中,此一控制亦能夠使熟諳此技藝者對他之製造過程的有效性具有自信,同時以該等微粒之細度及尺寸的觀點對該最終客戶保證精密之規格。In the field of powders, the control of particle size measurement is an essential element for those skilled in the art, an industrial process engineer who knows a lot of knowledge, and a technician who specializes in powder materials. In fact, in the case of mineral material powders, this control enables him to understand the quality of the products made in the course of the different stages of particle size reduction. In the more general field of dry powders, and especially in the field of mineral powders, plastic powders, metal powders, ceramic powders, or detergents, and sugars, this control can also be made by the skilled person. The effectiveness of the process is self-confident, while ensuring precise specifications for the end customer in terms of the fineness and size of the particles.
於該糖之領域中,其實已熟知的是該等個別結晶體之尺寸分佈影響由該等結晶體所形成的糖塊在水中之溶化,如於“糖之溶化”(1990年Zuckerindustrie Berlin、115(4)、第250-60頁)中所敘述者。In the field of sugars, it is well known that the size distribution of the individual crystals affects the melting of the sugar pieces formed by the crystals in water, such as "melting of sugar" (Zuckerindustrie Berlin, 1990 (4) ), as described in pages 250-60).
除了別的以外,該相同原理可應用於清洗粉蠟筆,其在水中之溶解性係藉著構成它們之個別微粒的尺寸分佈所影響,且該相同之因素亦影響該等粉末之流動性,如藉由該文件“使用氣壓噴嘴的顆粒狀洗衣清潔劑之生產”(Inzynieria i Aparatura Chemiczna(1996年),35(3),第15-18頁)所教導者。The same principle can be applied, among other things, to the cleaning of crayons whose solubility in water is affected by the size distribution of the individual particles constituting them, and the same factors also affect the fluidity of the powders, such as The document is taught by the document "Production of a granular laundry detergent using a pneumatic nozzle" (Inzynieria i Aparatura Chemiczna (1996), 35(3), pp. 15-18).
於陶瓷之領域中,其亦熟知的是一碳酸鈣粉末之粒度測量分佈能在該等粉末之流動能力性質上、或在包含該粉末的陶瓷材料之乾燥上具有一影響,如在“碳酸鈣片條熔煉本體的乾燥收縮率行為上之平均微粒尺寸的影響”(1998年(1999年)十月31日至十一月3日於中國北京市的高性能陶瓷上之第一屆中國國際會議的活動記錄,會議日期1998年第181-184頁)中所指示者。In the field of ceramics, it is also well known that the particle size distribution of a calcium carbonate powder can have an effect on the flowability properties of the powder or on the drying of the ceramic material comprising the powder, such as in "calcium carbonate. The effect of the average particle size on the drying shrinkage behavior of the strip smelting body" (The first China International Conference on High Performance Ceramics, Beijing, China, October 31-November 3, 1998 (1999) The record of the activity, as indicated in the date of the meeting, pages 181-184 of 1998).
於該塑膠工業中所使用之粉末領域,其亦已熟知此粒度測量分佈對該等粉末之流動性扮演一很重要之角色。該相同之原理可應用於金屬粉末。It is also well known in the field of powders used in the plastics industry that this particle size measurement distribution plays an important role in the fluidity of such powders. This same principle can be applied to metal powders.
最後,於該礦物工業中,其熟知的是粉末之此相同的粒度測量分佈係一根本因素,其能夠影響包含該等粉末、尤其以碳酸鈣為基礎之粉末的最終產品之很多性質。實際上,很多工作將微粒之尺寸的此分佈連結至碳酸鈣之溶化(“呈粉末形式的CaCO3 之溶化動力學及在溶化進程上之微粒尺寸及預處理的影響”,工業及工程化學研究,(1996年),35(2),第465-74頁)、連結至包含碳酸鈣的塑膠成份之機械性質(“在聚丙烯的流動學性質上之CaCO3 微粒尺寸分級的效果”,Feijinshukuang,(2001年),24(2),第13-14頁)、連結至以包含碳酸鈣的紙張塗層所製成之紙片的光學性質(“經研磨碳酸鈣之微粒尺寸應用在色彩流變學之效果及經塗附紙張之性質”,Kami Pa Gikyoshi,(1999年),53(9),第1174-1178頁)、或再次連結至包含碳酸鈣的塗料薄膜之結構(“使用水銀孔隙度測定法之塗料薄膜的結構上之天然碳酸鈣的微粒尺寸分佈之影響”,Double Liaison-Chimie des Peintures[Chemistry of Paints],(1986年),33(372),第25-37頁,VIII-XVIII)。Finally, in the mineral industry, it is well known that this same particle size measurement distribution of powders is a fundamental factor that can affect many of the properties of the final product comprising such powders, especially calcium carbonate based powders. In fact, many jobs link this distribution of particle size to the dissolution of calcium carbonate ("the melting kinetics of CaCO 3 in powder form and the effect of particle size and pretreatment on the melting process", industrial and engineering chemistry studies (1996), 35(2), pp. 465-74), mechanical properties linked to plastic components containing calcium carbonate ("Effects of CaCO 3 particle size grading on the flow properties of polypropylene", Feijinshukuang , (2001), 24(2), pp. 13-14), optical properties linked to paper sheets made from paper coatings containing calcium carbonate ("Poreed calcium carbonate particle size applied to color rheology "The effect of learning and the nature of coated paper", Kami Pa Gikyoshi, (1999), 53(9), pp. 1174-1178), or reattachment to the structure of a coating film containing calcium carbonate ("Using mercury pores" The influence of the particle size distribution of natural calcium carbonate on the structure of coating films by degree measurement", Double Liaison-Chimie des Peintures [Chemistry of Paints], (1986), 33 (372), pp. 25-37, VIII -XVIII).
為了控制該等粉末的粒度測量之目的,尤其於該礦物工業中,熟練於該技藝者必需因此具有一裝置:-其係在它之製造過程中易於安裝,且使用簡單;-其能於該礦物物質之粒度測量減少的製程中被線上地使用(以便在此製程中之一給定點控制其細度-典型在一研磨及/或選擇裝置之輸出);-其係與一生產場所之工業限制條件相容的(諸如有關研磨機之使用的震動、設備之各種項目的移動中所固有之衝擊、通常具有一高粉狀微粒含量之大氣等)。In order to control the particle size measurement of such powders, especially in the mineral industry, it is necessary for the skilled person to have a device which is easy to install during its manufacture and which is simple to use; The process of reducing the particle size measurement of mineral matter is used on-line (to control its fineness at a given point in the process - typically at the output of a grinding and / or selection device); - its industry with a production site The constraints are compatible (such as vibrations associated with the use of the grinder, impacts inherent in the movement of various items of equipment, atmospheres typically having a high particulate content, etc.).
為了記述各種粉末之粒度測量的特徵,其在一實驗室階段規模上係熟知使用諸如藉著傳送、藉著擴散之電子顯微鏡的技術、基於該氣體吸附之方法、基於愛克斯光繞射之光學資源、傳統之光學顯微鏡、或真正地雷射技術。如此,為了於該陶瓷領域中測量氧化鋁粉末之有特色的尺寸,該文件“各種微粒大小分級技術之比較”(武漢大學技術期刊,材料科學版本,2000年,第7-14頁)報告這些技術之使用。In order to characterize the particle size measurement of various powders, it is well known on a laboratory scale to use optical techniques such as by electron transfer through diffusion, methods based on the gas adsorption, optical resources based on Axel diffraction. , traditional optical microscopes, or true laser technology. Thus, in order to measure the distinctive dimensions of alumina powder in the ceramic field, the document "Comparison of various particle size grading techniques" (Wuhan University Technical Journal, Materials Science Edition, 2000, pp. 7-14) reports these Use of technology.
當作用於決定粉末之粒度測量分佈的商業設備之範例,並使用一些該先前論及之技術,該申請人能引用藉由MalvernTM 公司所製成之MastersizerTM 實驗室雷射粒度測量儀的範圍、藉由相同公司所製成之InsitecTM 線上雷射粒度測量儀的範圍、及藉由該Micromeritics公司所製成之SedigraphTM 型裝置,其技術係基於愛克斯光繞射。As examples of commercial equipment used to determine the particle size distribution of the powder is measured, and use some of the prior art addressed, the applicant can be cited range by a Malvern Mastersizer TM TM of the company made laser particle sizer of the laboratory , the range of the Insitec laser particle sizer TM made online by the same company, and by the company Micromeritics Sedigraph (TM) type made of apparatus, which is based on X-ray diffraction techniques.
如此,為了決定糖結晶體之尺寸,於藉由本發明所關心之領域中,該文件“蔗糖之酒精性結晶作用”(昆士蘭大學,化工科系之論文,1E0406/7,2000年)報告一MastersizerTM 粒度測量儀之使用。此相同之裝置已順利地被使用,以決定塑膠材料之粒度測量,如“一般使用之直接壓縮接合劑的物理性質及簡潔之分析”(AAPS PharmSciTech。2003年、4(4),第62條)中所敘述者。相同地,“氫氧基磷灰石之膠態處理”(生醫材料,22、2001、第1847-1852頁)有關一SedigraphTM 5100型裝置之使用,以決定該等陶瓷材料的製造中所使用之氫氧基磷灰石粉末的粒度測量分佈。So, in order to determine the size of the crystals of sugar, for by areas of concern of the present invention, the file (University of Queensland, chemical department of the paper, 1E0406 / 7, 2000) "alcoholic sucrose crystallization" Report a Mastersizer TM The use of a particle size measuring instrument. This same device has been successfully used to determine the particle size measurement of plastic materials, such as "analysis of the physical properties and simplicity of direct compression bonding agents commonly used" (AAPS PharmSciTech. 2003, 4(4), Article 62 The person described in ). Similarly, "colloidal processing of hydroxyapatite" (biomaterials, 22,2001, pp. 1847-1852) using a Sedigraph TM 5100 about the type of device to determine the manufacturing of ceramic materials such as The particle size distribution distribution of the hydroxyapatite powder used.
其係亦已知基於使用照相機所進行之影像的分析在粉末粒度測量的一般領域中使用測量裝置。熟練於該技藝者係熟悉此領域,並具有藉由該Retsch TechnologyTM 公司所銷售之名稱為CamsizerTM 的設備、藉由Haver及BoeckerTM 公司所銷售之CPATM 、或又藉由Norske HydroTM 公司所銷售之Part AnTM 。It is also known to use measurement devices in the general field of powder particle size measurement based on analysis of images performed using a camera. Those skilled in the art department familiar with this area, and has a name by the Retsch Technology TM company sold the equipment to Camsizer TM, by Haver and Boecker TM sold the company's CPA TM, or by another company Norske Hydro TM Part An TM sold.
然而,此等裝置具有許多缺點。視該等裝置而定,其粒度測量之測量範圍係狹窄的。這些裝置專攻一測量範圍。它們不能立刻測量遍及數十微米至數毫米之範圍。經過諸如雷射、照相機等技術之使用,該等結果係由統計之計算所推得:它們需要藉著相互關係作調整,這花費相當可觀之時間以計算。該統計方法不能夠給與該乘積之百分率,其對於所運送產品之品質係必要的。此外,這些精確裝置係難以順應某些項目之設備、諸如研磨機的存在所固有之震動,該等研磨機在該礦物工業中係時常發現。這些震動亦干擾該等裝置,其粒度測量之測量範圍係較寬廣的,諸如藉著影像分析之光學系統,由於其景深過度淺之結果,其不能夠獲得一需要之影像品質,以充分記述所產生粉末之特徵,除了藉著使用顯微測量之影像細化技術以外,其於一受限制之工業環境(震動等)中係不穩定的。However, such devices have a number of disadvantages. Depending on the device, the measurement range of the particle size measurement is narrow. These devices specialize in a measurement range. They cannot be measured immediately over a range of tens of microns to a few millimeters. Through the use of technologies such as lasers and cameras, these results are derived from statistical calculations: they need to be adjusted by interrelationships, which takes considerable time to calculate. This statistical method cannot give the percentage of the product, which is necessary for the quality of the delivered product. Moreover, these precision devices are difficult to comply with the vibrations inherent in the equipment of certain items, such as the presence of grinders, which are often found in the mineral industry. These vibrations also interfere with such devices, and the measurement range of the particle size measurement is relatively wide. For example, an optical system by image analysis cannot obtain a desired image quality due to its excessive depth of field, so as to fully describe the The characteristics of the resulting powder, except by the use of microscopic measurement of image refinement techniques, are unstable in a restricted industrial environment (vibration, etc.).
此外,若干裝置係相當昂貴的;它們在嚴苛之清潔條件之下,使用需要供分析之樣本的通常係冗長及過分精細之調整的技術,在一礦物物質製造單元之情形(大氣中存在有粉狀物質)中,其有時候係難以獲得。再者,某些技術能夠記述僅只極少量(數公克)之粉末的特徵,這造成該等樣本相對大部分工業設備的實際生產能力之代表性的問題。最後,這為著該等已製成粉末之粒度測量的線上測量之目的,些測量裝置-本身-將必需遭受很多修改,以便在該製造過程中之一精確地點使用,其對於該等熟練於該技藝者構成該主要之需求。In addition, several devices are quite expensive; they use techniques that are typically lengthy and excessively fine adjustments of the sample to be analyzed under severe cleaning conditions, in the case of a mineral material manufacturing unit (there is Among the powdery substances, it is sometimes difficult to obtain. Moreover, certain techniques are capable of characterizing only a very small amount (a few grams) of powder, which poses a problem of the representativeness of the actual production capacity of such samples relative to most industrial equipment. Finally, for the purpose of on-line measurement of the particle size measurement of these already made powders, some measuring devices - by themselves - will have to undergo many modifications in order to be used at one precise location in the manufacturing process, which is proficient for such The artist constitutes this primary need.
因此,基於其尺寸、使用機械裝置、基於篩子、篩網、網織品、或彈簧之任一種,熟練於該技藝者寧願基於微粒之選擇而選擇涉及特徵記述之設備。於這些類別之每一種中,該申請人將現在回顧熟練於該技藝者可取得之文件。Therefore, based on its size, the use of mechanical devices, sieves, screens, nets, or springs, those skilled in the art would prefer to select devices that involve feature description based on the choice of particles. In each of these categories, the Applicant will now review the documents available to those skilled in the art.
基於篩子、篩網及網織品的裝置之類別係非常大的。如此,該申請人指示該國際專利分類(第八修訂版)之B07B級在本申請案之存檔日期包含超過17,789文件,其有關篩子、篩網、及使用網織品、格柵的固體材料之分類或可比較之系統。The types of devices based on screens, screens and nets are very large. Thus, the applicant indicates that the B07B level of the International Patent Classification (eighth revision) contains more than 17,789 documents on the filing date of this application, relating to sieves, screens, and solid materials using nettings and grilles. Classification or comparable system.
然而,在它們之中,其係可能使用不同幾何形狀之轉動及/或震動篩網區別裝置。如此,美國專利文件第US 4 184 944號敘述一圓柱形篩網裝置,其連續地繞著其水平軸心轉動,且能夠使粉末乾燥或潮濕至經過圍繞該圓柱體之篩網篩選。同時,歐洲專利文件EP1 163 958號呈現一圓柱形裝置,其在其水平軸心連續地轉動,在此該水平移動係藉著一施加至形成該圓柱體的篩網之振動性移動所完成:此裝置係特別意欲用於篩選以泥土為基礎之材料。Among them, however, it is possible to use different geometrically shaped rotating and/or vibrating screens to distinguish devices. Thus, U.S. Patent No. 4,184,944 describes a cylindrical screen apparatus which is continuously rotated about its horizontal axis and which is capable of drying or damping the powder to screen through a screen surrounding the cylinder. At the same time, the European patent document EP 1 163 958 presents a cylindrical device which continuously rotates at its horizontal axis, where the horizontal movement is accomplished by a vibrating movement applied to the screen forming the cylinder: This device is specifically intended for screening soil-based materials.
大致上,該申請人指示該圓柱形罐籠之使用,該罐籠覆蓋著一篩網,隨著一旋轉式及/或振動性移動而移動,如此能夠篩選礦物之微粒,且係熟諳此技藝者所熟知之機構。其次,除了該等上述裝置以外,其常見的是以此方式稱重該等已篩選之材料,該方式係能夠獲得諸微粒的一質量比率,該等微粒之直徑係少於所使用之篩網的篩孔。然而,這些裝置不會讓熟諳此技藝者滿意,因為它們被工業地用於分開不同本質之材料及/或清洗藉由非常不同的粒度測量之微粒所污染的材料。因此,它們不欲用於記述粉末之特徵。此外,這些裝置係裝配有覆蓋其整個圓周的單一型式之篩網,並僅只能夠記述單一粒度測量等級之微粒的特徵。此外,這些裝置沒有任一個顯露出能夠線上地測量粉末之粒度測量的系統。In general, the Applicant indicates the use of the cylindrical cage, which is covered with a screen and moves with a rotary and/or vibrating movement so as to be able to screen mineral particles and is familiar to the skilled person. A well-known institution. Secondly, in addition to the above-mentioned devices, it is common to weigh the screened materials in such a manner that a mass ratio of the particles is obtained, the diameter of the particles being less than the screen used. Screen hole. However, these devices are not satisfactory to those skilled in the art because they are used industrially to separate materials of different nature and/or to clean materials contaminated with particles measured by very different particle sizes. Therefore, they are not intended to describe the characteristics of the powder. Moreover, these devices are equipped with a single type of screen covering the entire circumference thereof and are only capable of characterizing the particles of a single particle size measurement. Moreover, none of these devices expose systems that measure the particle size of the powder on-line.
在基於篩子、篩網或其他格柵的裝置之類別中,該申請人最後係熟悉美國專利文件第US 4 487 323號,其敘述一裝置,以基於一繞著其水平軸心轉動之鼓輪記述粉末之粒度測量的特徵,其具有一開口及不同之篩網。該鼓輪環繞著其軸心移至不同位置,且係藉著一震動馬達所攪動,其允許該粉末之篩選,該粉末包含經過該篩網之粉末,該粉末係往下引導。一位於該鼓輪下方及由該系統分開之天平能夠使已通過每一篩網的微粒之質量被量化。然而,此一裝置不能夠線上地記述粉末之粒度測量的特徵,因為該操作員必需手動地放置該粉末供在該鼓輪內之測試。In the category of devices based on screens, screens or other grids, the applicant is finally familiar with U.S. Patent No. 4,487,323, the disclosure of which is incorporated herein incorporated by its entirety in The characteristics of the particle size measurement of the powder are described, which have an opening and a different screen. The drum is moved to its different positions around its axis and is agitated by a vibration motor that allows screening of the powder, the powder comprising powder passing through the screen, the powder being directed downward. A balance located below the drum and separated by the system enables the mass of particles that have passed through each screen to be quantified. However, such a device is not capable of characterizing the particle size measurement of the powder on-line because the operator must manually place the powder for testing within the drum.
該等熟諳此技藝者因此轉向用於測量粉末之粒度測量的裝置之類別,尤其經過彈簧之使用。Those skilled in the art therefore turn to the category of devices for measuring the particle size measurement of powders, especially through the use of springs.
此技術其實近來比在上方所論及者(且其係基於格柵、篩網或篩子)出現更多。因此,其包含的文件之數目係遠較小,且其對於熟諳此技藝者迅速地認知諸裝置係更容易的,於其製造過程期間,該等裝置盡可能地使他能夠解決線上地記述不同粉末之粒度測量的特徵之問題。This technique has actually appeared more recently than it has been discussed above (and it is based on grids, screens or screens). Therefore, the number of files it contains is much smaller, and it is easier for those skilled in the art to quickly recognize the devices, and during their manufacturing process, the devices are as capable as possible to solve the problem of being written online as much as possible. The problem of the characteristics of the particle size measurement of the powder.
如此,熟諳此技藝者迅速地認知該近來之美國專利文件第US 6 829 955 B1號(2004年12月14日發表之美國專利)。此文件敘述一允許線上地、及以一相當簡單之方式決定各種粉末的粒度測量之裝置。此一裝置係裝配有一彈簧,該彈簧的諸線圈之間隔將能夠使微粒之不同粒度測量類別通過,該間隔根據該彈簧之振動的振幅而變化。然而,此一裝置對於熟諳此技藝者仍然造成新的問題,雖然其確實已能夠線上地記述各種粉末之粒度測量的特徵。實際上,如該文件之封面頁的概要圖所指示,當待分析粉末之微粒落入位在該彈簧上方之承接室時,它們造成一雙重之缺點:其能量可為充分大,使得當它們與該彈簧撞擊時改變它們(不再保證供測試之材料的完整性),及/或藉著損壞該等線圈或藉著改變其間隔使得它們損壞該彈簧(不再保證該裝置的完整性,且因此不再保證該測量的完整性)。Thus, the skilled person is acquainted with the recent U.S. Patent No. 6,829,955 B1 (issued on December 14, 2004). This document describes a device that allows for the determination of the particle size of various powders on-line and in a relatively simple manner. This device is equipped with a spring whose spacing of the coils will enable the passage of different particle size measurement categories of particles which vary according to the amplitude of the vibration of the spring. However, such a device still poses new problems for those skilled in the art, although it has indeed been able to characterize the particle size measurement of various powders on-line. In fact, as indicated by the overview of the cover page of the document, when the particles of powder to be analyzed fall into the receiving chamber above the spring, they create a double disadvantage: their energy can be sufficiently large that when they Changing them when impacted by the spring (no longer guaranteeing the integrity of the material being tested), and/or damaging the spring by damaging the coils or by changing their spacing (the device is no longer guaranteed to be complete, And therefore the integrity of the measurement is no longer guaranteed).
因此,為了解決他之最初技術問題,在於開發一用於線上地記述粉末之粒度測量的特徵之裝置,該裝置係在工業中係安裝簡單,且與該等工業之限制條件、諸如震動相容,該申請人已經開發一裝置,其同時滿足這些條件,克服關於構成該最近之先前技藝的美國專利文件第US 6 829 955號之缺點,因為其已經解決該最初之技術問題,這些缺點係用於分析的材料之改變及對該測量裝置之損壞。Therefore, in order to solve his original technical problem, it is to develop a device for describing the characteristics of the particle size measurement of the powder on-line, which is simple to install in the industry and compatible with such industrial constraints, such as vibration. The Applicant has developed a device that satisfies these conditions at the same time, overcoming the shortcomings of U.S. Patent No. 6,829,955, which is incorporated herein by reference. Changes in the material being analyzed and damage to the measuring device.
根據本發明的裝置之發展顯現為特別有創造力的,因為其絕未依賴構成該技術之最近狀態的文件,而該等熟諳此技藝者將已必需尋求該文件,以用一明顯及天然之方式作改善。The development of the device according to the invention appears to be particularly creative, since it never relies on documents that constitute the most recent state of the technology, and those skilled in the art will have to seek the document to use an obvious and natural Ways to improve.
反之,以一完全有創造力的方式,該申請人已在一很大組文件之中順利地認知一更加老舊之文件,即美國專利文件第4 487 323號,因為此專利文件有關一包括基於篩子、篩網或格柵之裝置的文件(國際專利分類的B07B級中之在2006年5月8日存檔的17,789文件),其所具有之操作已經大幅地轉變,以便解決其技術問題。Conversely, in a completely creative manner, the applicant has successfully recognized an older document in a larger set of documents, namely U.S. Patent No. 4,487,323, which is incorporated herein by reference. Documents based on sieves, screens or grids (17,789 files filed on May 8, 2006 in the B07B level of the International Patent Classification) have significantly changed their operations in order to solve their technology. problem.
此文件之選擇對於該等熟諳此技藝者係較不正常/明顯的,因為如先前已敘述者,該美國專利文件第4 487 323號未解決在本申請案中所造成的最初之技術問題。實際上,該申請人係渴望強調使用美國專利文件第4 487 323號中所敘述之裝置不能達成線上地記述粉末之粒度測量的特徵。實際上,為了記述粉末之粒度測量的特徵,在該文件中需要數項人類之介入:將該粉末導入該篩選鼓輪,尤其是在此導入之過程期間冒著該等篩網將被損壞(且因此手動地改變該等篩網)或阻塞(且因此手動地清洗該等篩網)之風險,及/或該粉末當其與該等篩網造成接觸(與接著該粉末之移除、該等篩網之手動清潔、及該粉末之新的導入以重新開始測量)時將被改變之風險、及該裝置、且尤其該等篩網之清潔/一般維護。反之,形成本發明之主題的裝置於該篩選循環期間不需要任何手動介入(然而,不會損壞/阻塞該等篩網、或修改該粉末),也不用清洗該等篩網。此外,其係裝配有一進給機構,該進給機構能夠使其直接由其製造過程收集(譬如由一給料斗,或由圓筒形密閉貯倉收集)用於分析之粉末:使得該裝置可與該粉末之製造的實際過程完美地同步化。The selection of this document is less than normal/obvious to those skilled in the art, as the prior art problems caused by the present application are not addressed in the U.S. Patent No. 4,487,323. In fact, the applicant is eager to emphasize the use of the device described in U.S. Patent No. 4,487,323, which is not capable of achieving the feature of the particle size measurement of the powder on-line. In fact, in order to characterize the particle size measurement of the powder, several human interventions are required in the document: the powder is introduced into the screening drum, especially during the introduction of the screen, the screen will be damaged ( And thus the risk of manually changing the screens or clogging (and thus manually cleaning the screens), and/or the powder when it comes into contact with the screens (and then the removal of the powder, The risk of changing the manual cleaning of the screen, and the new introduction of the powder to restart the measurement, and the cleaning/general maintenance of the device, and in particular the screens. Conversely, devices forming the subject of the present invention do not require any manual intervention during the screening cycle (however, the screens are not damaged/blocked, or the powder is modified) and the screens are not cleaned. Furthermore, it is equipped with a feed mechanism which enables it to be collected directly from its manufacturing process (for example by a feed hopper or by a cylindrical closed silo) for the analysis of the powder: making the device It is perfectly synchronized with the actual process of manufacture of the powder.
在已順利地認知此文件之後,該申請人亦順利地修改藉著該文件所涵蓋之裝置,以便:-解決其最初之技術問題(亦即使線上地決定粉末之粒度測量成為可能,並以一與該等工業限制條件、諸如震動相容之簡單的方式);-同時解決此最初之技術問題,避免有關用於測試的材料之改變及對該測量裝置之損壞的缺點,即在美國專利文件第US 6 829 955號中所顯示之缺點。After having successfully recognized this document, the applicant has also successfully modified the device covered by the document to: - solve its original technical problems (even if it is possible to determine the particle size measurement of the powder online, and A simple way to comply with such industrial constraints, such as vibration); - simultaneously solve this initial technical problem, avoiding the shortcomings of the material used for testing and the damage to the measuring device, ie in the US patent document Disadvantages shown in US Pat. No. 6,829,955.
因此,為了解決其最初之技術問題,亦即以一與工業限制條件相容之簡單方式使線上地決定粉末之粒度測量成為可能,該申請人已經導入一進給機構,其能夠使用於測試之粉末被直接導入該水平篩選機構;一機構,其未包含於美國專利文件第4 487 323號中。此一選擇將不可避免地導致用於分析的粉末之突然抵達該等篩網上,導致該粉末將被改變及/或該等篩網將被損壞之可能性:因此發現在美國專利文件第US 6 829 955號中所造成之問題,示範此選擇不是正常的。因此,該申請人功績之一有關該方式,其中其能夠解決該後面之缺點:其裝配有該水平篩選機構,該水平篩選機構設有一抗撞擊板件,該抗撞擊板件未包含於美國專利文件第4 487 323號中,該板件具有一抗衝擊特性,因為其在該測量循環之最初係定位在該最低位置,以承接用於測試之粉末。使得該等篩網不再被損壞及用於測試之粉末不再被改變,確保兩者之完整性。該抗衝擊板件其實係一裝配有墊子之不銹鋼機架,該墊子係由一天然橡膠(高耐磨性)及一聚矽氧膠化體所製成。膠化體之特別的特色係其藉著吸收該衝擊之能量防止該產品之任何彈回作用,而不會使其返回。Therefore, in order to solve its original technical problem, that is, to make it possible to determine the particle size measurement of the powder online in a simple manner compatible with industrial constraints, the applicant has introduced a feeding mechanism which can be used for testing. The powder is introduced directly into the level screening facility; an institution that is not included in U.S. Patent No. 4,487,323. This choice will inevitably result in the sudden arrival of the powder for analysis on the screens, resulting in the possibility that the powder will be altered and/or the screens will be damaged: thus found in US Patent Document No. US The problem caused by No. 6 829 955, the demonstration of this choice is not normal. Therefore, one of the applicant's merits relates to the method in which it can solve the latter drawback: it is equipped with the horizontal screening mechanism, which is provided with an anti-impact plate member, which is not included in the US patent. In document No. 4,487,323, the panel has an impact resistance feature because it is initially positioned at the lowest position during the measurement cycle to receive the powder for testing. The screens are no longer damaged and the powder used for testing is no longer altered to ensure the integrity of both. The impact plate is actually a stainless steel frame equipped with a mat made of a natural rubber (high abrasion resistance) and a polyoxylized gel. A particular feature of the gelled body is that it absorbs the energy of the impact to prevent any rebound of the product without returning it.
因此,經過本發明,該等熟諳此技藝者具有一裝置,其能夠線上地記述粉末之特徵,該裝置之使用係簡單的,並與一工業生產單元中所存在之震動相容,其不會改變用於分析的粉末,且其在與該粉末接觸時不會造成損壞:這構成用於該等熟諳此技藝者之主要需求。Thus, through the present invention, those skilled in the art have a device capable of describing the characteristics of the powder on-line, the device being simple to use and compatible with the vibrations present in an industrial production unit, which will not The powder used for the analysis is altered and does not cause damage upon contact with the powder: this constitutes a major need for those skilled in the art.
最後,在此有藉由本發明所獲得之二項其他次要優點,該等優點係未被美國專利文件第4 487 323號所提供。該申請人強調這些2其他優點未與該新的技術問題有關,因為它們能被連結至該最初之技術問題,如先前所呈現者。就其解決方法僅只構成本發明之選擇性特徵的意義來說,該申請人已僅只選擇呈現它們當作次要之技術問題。Finally, there are two other minor advantages obtained by the present invention which are not provided in U.S. Patent No. 4,487,323. The Applicant emphasizes that these two other advantages are not related to this new technical issue as they can be linked to the original technical issue, as previously presented. Insofar as the solution only constitutes a selective feature of the invention, the Applicant has only chosen to present them as secondary technical issues.
就該測量機構係一由該裝置之其餘部份分開的零件之意義來說,該第一項係在美國專利文件第4 487 323號中所敘述之裝置係不易於使用:如果吾人想要移動該裝置,該測量機構必需因此被移動,這需要一成對的操作。並將該測量機構緊繫至該裝置之其餘部份將使得其與藉由該連續震動機構所造成之震動相依,且因此未能提供一可靠之測量。在此該申請人之另一功績係基於其已經施行之解決方法,及其在於將該測量機構有效地緊繫至該裝置之其餘部份,但其亦在於在該馬達及該篩選機構的水平軸心之間安裝一彈性耦接機構。以此方式,此組合能夠供給形成單一零件之裝置(在該工廠中不須多數操作供移動之),且延長該裝置之震動機構的使用壽命。實際上,因為該震動系統能夠藉著施加震動至耦接至該震動系統之軸心而使該轉動罐籠震動,該申請人順利觀察到以下之事實,即藉著一彈性耦接機構打斷該軸心/馬達連結,該彈性耦接機構能夠避免將該震動傳送至該馬達:藉著此機構,該馬達之使用壽命係增加。此彈性耦接機構尤其可為一以彈性體為基礎之機構,其對於該等熟諳此技藝者係熟知的。In the sense that the measuring mechanism is a part separated by the rest of the device, the device described in the first item in the U.S. Patent No. 4,487,323 is not easy to use: if I want to move The device, the measuring mechanism must therefore be moved, which requires a pair of operations. Tightening the measuring mechanism to the rest of the device will cause it to be dependent on the vibrations caused by the continuous vibrating mechanism and thus fail to provide a reliable measurement. Here, another merit of the applicant is based on the solution that has been implemented, and that the measuring mechanism is effectively tied to the rest of the device, but also at the level of the motor and the screening mechanism. An elastic coupling mechanism is installed between the shaft centers. In this way, the combination can supply a device that forms a single part (without requiring a large amount of operation for movement in the plant) and extending the useful life of the vibrating mechanism of the device. In fact, because the vibration system is capable of vibrating the rotating cage by applying vibration to the axis coupled to the vibration system, the applicant successfully observed the fact that the elastic coupling mechanism interrupts the A shaft/motor linkage that avoids transmitting the shock to the motor: by this mechanism, the life of the motor is increased. This resilient coupling mechanism can be, inter alia, an elastomer-based mechanism that is well known to those skilled in the art.
該第二項有關使用之簡化的需求,及有關該裝置之清洗。在此,該申請人之功績係基於以下之事實,即其已能夠觀察到一包括至少一噴嘴及/或一超音波發生器之自動清洗機構,該超音波發生器位於該篩選機構之周邊上,且將壓縮空氣投射在該篩網上將能夠與該等篩網之一或更多旋轉操作結合,以在一很短之時間內完全及完美地清潔該整個裝置。This second item relates to the simplified requirements for use and to the cleaning of the device. Here, the applicant's merits are based on the fact that it has been able to observe an automatic cleaning mechanism comprising at least one nozzle and/or an ultrasonic generator located on the periphery of the screening mechanism. And projecting compressed air onto the screen will enable one or more rotational operations in conjunction with the screens to completely and perfectly clean the entire apparatus in a short period of time.
最後,該申請人係渴望指示其以該先前技藝之觀點係對該法國專利第05 04917號熟悉的,且因此僅只關於新穎之事物來至該技術之狀態內(根據知識產權守則之L611-14條款及亦根據歐洲專利公約之54(2)條款)。然而,除了別的以外,在此於該申請案及本發明之間有一基本之差異,於該旋轉機構之4位置中,在本發明之情況中,該等位置之一係一抗衝擊板件。因此,本發明之第一目的係一用於記述粉末之粒度測量的特徵之裝置,其具有一進給機構、一排空機構、一稱重機構、一連續震動機構、一篩選機構、及一可能有之控制機構,且其特徵為:-其中該篩選機構係一繞著水平軸心轉動之機構,具有用於一未被佔用的空間或一用於粉末之釋放及導入的空間之至少1位置、用於一抗衝擊板件之1位置、用於不同篩孔之2篩網的至少2位置;-及其中該裝置具有一清潔機構,該清潔機構由至少一噴嘴及/或一位在該篩選機構的周邊上之超音波發生器所組成;-及其中該裝置具有一彈性耦接機構,其位在該篩選機構的水平軸心與該連續震動機構之間。Finally, the applicant is eager to indicate that it is familiar with the French patent No. 05 04917, and therefore only relates to novelty to the state of the technology (according to the Intellectual Property Code L611-14) The terms and conditions are also in accordance with Article 54(2) of the European Patent Convention). However, there is, among other things, a fundamental difference between the application and the present invention, in the position 4 of the rotating mechanism, in the case of the present invention, one of the positions is an impact resistant plate . Accordingly, a first object of the present invention is a device for describing characteristics of particle size measurement of a powder, comprising a feed mechanism, an emptying mechanism, a weighing mechanism, a continuous vibration mechanism, a screening mechanism, and a There may be a control mechanism, and is characterized in that: - the screening mechanism is a mechanism that rotates about a horizontal axis, and has at least one space for an unoccupied space or a space for release and introduction of powder. Position, at a position of 1 for an impact resistant panel, at least 2 positions for a screen of 2 different screen openings; and wherein the device has a cleaning mechanism consisting of at least one nozzle and/or one An ultrasonic generator on the periphery of the screening mechanism; and wherein the device has an elastic coupling mechanism between the horizontal axis of the screening mechanism and the continuous vibration mechanism.
該裝置係因此裝配有一進給機構(1),用於分析之粉末經過該進給機構進入該篩選機構(2)。該等熟諳此技藝者將能夠設計該進給機構,以便將其連結至一圓筒形密閉貯倉、一給料斗、或用於測試之粉末的製造過程中之任何其他地點,以便在該地點對該粉末抽樣,為了將其運送進入形成本發明之主題的裝置。The device is thus equipped with a feed mechanism (1) through which the powder for analysis enters the screening mechanism (2). Those skilled in the art will be able to design the feed mechanism to connect it to a cylindrical closed silo, a hopper, or any other location in the manufacturing process for the powder to be tested, so that at that location The powder is sampled for transport into a device that forms the subject of the present invention.
藉著此方法,其係可能線上地決定用於測試的粉末之粒度測量,其係本發明的優點之一。By this method, it is possible to determine the particle size measurement of the powder for testing on the line, which is one of the advantages of the present invention.
該篩選機構係一繞著其水平軸心(3)轉動之機構,且於此圖面中,既未示出該自由空間、該等不同篩網,也未示出該抗衝擊板件,該抗衝擊板件形成該篩選機構的特徵之一部份(將參考圖2,在上面已詳細地敘述)。該連續震動機構(4)將其震動賦予至該軸心(3),並將震動傳送至該篩選機構。該彈性耦接機構(5)限制該篩選機構的震動之傳播至該連續震動機構:該連續震動機構之使用壽命係藉著此方式所增加。The screening mechanism is a mechanism that rotates about its horizontal axis (3), and in this drawing, the free space, the different screens, and the impact plate are not shown, The impact resistant panel forms part of the features of the screening mechanism (refer to Figure 2, which has been described in detail above). The continuous vibration mechanism (4) imparts its vibration to the axis (3) and transmits the vibration to the screening mechanism. The elastic coupling mechanism (5) limits the propagation of the vibration of the screening mechanism to the continuous vibration mechanism: the service life of the continuous vibration mechanism is increased by this means.
藉著此方式,吾人具有一形成單一部件之裝置,亦即一使用簡單及尤其在一製造廠移動簡單之裝置,且該裝置之連續震動機構的使用壽命係延長:這構成本發明的諸優點之一。In this way, we have a device that forms a single component, that is, a device that is simple to use and that is particularly easy to move in a manufacturing plant, and that the service life of the continuous vibration mechanism of the device is extended: this constitutes the advantages of the present invention. one.
用於分析之不同粒度測量等級的微粒經過該篩選機構之篩網、經過該排空機構(6)流出,且其重量最後係於該稱重機構(7)中量化。The particles of different particle size measurement levels for analysis pass through the screen of the screening mechanism, flow out through the evacuation mechanism (6), and the weight is finally quantified in the weighing mechanism (7).
圖2概要地說明該圓柱形篩選機構,事實上其尤其可能根據圖1之剖面AA作觀察。Figure 2 schematically illustrates the cylindrical screening mechanism, in fact it is particularly possible to observe from section AA of Figure 1.
在記述該粉末之特徵的循環期間,配置該篩選機構,使得該抗衝擊板件(a)係定位在該最低位置。以此方式,用於測試之粉末直接經過開口(e)抵達在此板件(a)上:該等材料不會被改變(尤其它們在與硬式篩網接觸時不會被打斷,如於該先前技藝之案例中),也不會讓它們損壞該等篩網(於該先前技藝之案例中):藉著此方法,用於分析的粉末之完整性、及該測量裝置之完整性、及尤其該等篩網尤其被保存。這是由本發明所提供之主要優點。During the cycle in which the characteristics of the powder are described, the screening mechanism is configured such that the impact resistant panel (a) is positioned at the lowest position. In this way, the powder used for testing arrives directly on the plate (a) through the opening (e): the materials are not altered (especially they are not interrupted when in contact with the hard screen, as in In the case of the prior art), they are not allowed to damage the screens (in the case of the prior art): by this method, the integrity of the powder used for the analysis, and the integrity of the measuring device, And especially such screens are especially preserved. This is a major advantage provided by the present invention.
實際上,該裝置保存用於分析的粉末之完整性,且不會藉著該粉末所損壞。在用於分析之材料的繼續完整性之主題上,該申請人係渴望強調這是一本質上之需求,以便不會扭曲該稱重測量。但盡可能地(及這亦是本發明之次要優點),該粉末抵達該抗衝擊板件、而不會損壞該抗衝擊板件之事實可譬如能夠於存在該板件上之該粉末造成另一非破壞性測量,諸如及不會希望為限制性的,一光學測量、諸如一彩色測量,其於諸如碳酸鈣的礦物物質之案例中有點特別重要。此外,本裝置不會具有先前論及的實驗室方法之缺點,因為其製造係不貴的,安裝及使用簡單,且因為其使用條件係完全與其被使用之工業環境相容的(大氣富含粉狀材料、衝擊、震動等)。In fact, the device preserves the integrity of the powder used for analysis and is not damaged by the powder. On the subject of continued integrity of the materials used for analysis, the Applicant is eager to emphasize that this is an essential requirement so as not to distort the weighing measurement. However, as far as possible (and this is also a secondary advantage of the present invention), the fact that the powder reaches the impact resistant panel without damaging the impact resistant panel can be caused, for example, by the presence of the powder on the panel. Another non-destructive measurement, such as and not intended to be limiting, an optical measurement, such as a color measurement, is somewhat of particular importance in the case of mineral materials such as calcium carbonate. In addition, the device does not have the disadvantages of the previously discussed laboratory methods because it is inexpensive to manufacture, simple to install and use, and because its conditions of use are completely compatible with the industrial environment in which it is used (atmospherically rich) Powdery materials, impact, vibration, etc.).
此外,不像該先前技藝之其他機械裝置,其能夠於單一操作(不會改變篩網或中斷該測量循環)中,記述微粒之數個粒度測量等級的特徵。最後,其簡化性使得其完美地被設計成適用於該礦物物質的製造過程中之任何地點,藉著此機制允許該等微粒之粒度測量的線上地控制,這對於該等熟諳此技藝者係基本之目標。Moreover, unlike other mechanical devices of the prior art, it is possible to characterize the number of particle size measurement levels of the particles in a single operation (without changing the screen or interrupting the measurement cycle). Finally, its simplification makes it perfectly designed to be suitable for use in any location in the manufacturing process of the mineral material, by which the on-line control of the particle size measurement of the particles is allowed, which is familiar to those skilled in the art. The basic goal.
該特徵記述循環能接著開始。一旦所有用於分析之粉末已被自動地放置在該抗衝擊板件上,該篩選機構係旋轉,直至緊接坐落位於相鄰該抗衝擊板件之最細篩孔篩網(b)係在該最低位置:接著篩選粉末微粒之第一粒度測量等級。對於緊接坐落相鄰該篩網(b)之篩網(c)重複該操作,且該篩網(c)具有一比該篩網(b)較大之篩孔,並接著對於篩網(d)重複該操作,該篩網(d)緊接坐落相鄰該篩網(c),且該篩網(d)具有一比該篩網(c)較大之篩孔。最後,在一最後的旋轉之後,該旋轉機構被定位,使得該沒有利用的空間係定位在該最低位置:停留於該圓柱體中之微粒係因此往下排空,且在該天平上稱重。This feature description loop can then begin. Once all of the powder used for analysis has been automatically placed on the impact resistant panel, the screening mechanism is rotated until the finest mesh screen (b) located adjacent to the impact resistant panel is attached The lowest position: the first particle size measurement level of the powder particles is then screened. This operation is repeated for the screen (c) located immediately adjacent to the screen (b), and the screen (c) has a larger screen than the screen (b), and then for the screen ( d) Repeating the operation, the screen (d) is immediately adjacent to the screen (c), and the screen (d) has a larger screen than the screen (c). Finally, after a final rotation, the rotating mechanism is positioned such that the unused space is positioned at the lowest position: the particles that remain in the cylinder are therefore emptied downwards and weighed on the balance .
此圖面因此代表根據本發明之裝置,其裝配有不同篩孔(b、c及d)之3個篩網;此數目係非限制性的,且其已回想形成本發明之主題的裝置必需具有不同篩孔之至少2篩網。該裝置被設計成可管理數個位置,且因此數個篩網適合用於控制分析用之粉末的製造過程。This figure thus represents a device according to the invention which is equipped with 3 screens of different mesh openings (b, c and d); this number is not limiting and it has been recalled that a device forming the subject of the invention is required At least 2 screens with different mesh openings. The device is designed to manage several locations, and thus several screens are suitable for controlling the manufacturing process of the powder for analysis.
藉著此機制,由於藉由該篩選機構環繞著其水平軸心所採用之連續位置,該等微粒被傳送至具有逐漸大的篩孔之篩網上:藉著此機制完成以尺寸分類該等微粒。與該裝置相連之稱重系統能夠測量該等微粒之質量,該等微粒之直徑係少於該等篩網的每一個之篩孔:藉著此機制,藉著報告微粒之每一質量,如該樣本之總重量的一函數,獲得該等微粒之粒度測量分佈。所獲得之結果能被表達為“通過”(橫越該篩網的微粒之百分比),表達為“拒絕”(停留於該篩網中之百分比,亦即與該“通過”相反),或根據此型式之結果的表達之任何其他機制。By this mechanism, due to the continuous position of the screening mechanism around its horizontal axis, the particles are transported to a screen having progressively large mesh openings: by means of this mechanism, the classification is done by size particle. A weighing system coupled to the apparatus is capable of measuring the mass of the particles, the diameter of the particles being less than the mesh of each of the screens: by this mechanism, by reporting each mass of the particles, such as A function of the particle size of the particles is obtained as a function of the total weight of the sample. The results obtained can be expressed as "pass" (percentage of particles across the screen), expressed as "rejected" (percentage of staying in the screen, ie opposite to "pass"), or according to Any other mechanism for the expression of the results of this pattern.
在用於記述該樣本之特徵的循環之尾端,該樣本於本發明之自動清洗操作(一已知為“逆流洗滌”之操作)期間被送回進入該製造循環。此清洗階段之目標係排空存在於該稱重機構中之粉末,以清潔該篩選機構之篩網,由該整個裝置移去灰塵,及重新恢復該裝置(隨著本發明的一可能故障之後用於啟動及/或恢復之開始位置,或在本發明之使用期間用於開始一新的循環之備用位置)。At the end of the cycle for characterizing the sample, the sample is returned to the manufacturing cycle during the automatic cleaning operation of the present invention (an operation known as "countercurrent washing"). The goal of this cleaning stage is to empty the powder present in the weighing mechanism to clean the screen of the screening mechanism, remove dust from the entire device, and reinstate the device (with a possible failure of the present invention) The starting position for starting and/or restoring, or the alternate position for starting a new cycle during use of the present invention).
其包括:-打開該稱重機構,以排空該樣本。It includes: - opening the weighing mechanism to empty the sample.
-將該篩選機構旋轉經過一或多圈。- Rotate the screening mechanism through one or more turns.
-將壓縮空氣投射在該等旋轉篩網上,尤其經過位於該篩選機構的任一側面上之噴嘴,如在圖2(f)中所表示,或將藉著位於該篩選機構的任一側面上之發生器所產生的超音波投射在該等旋轉篩網上。- projecting compressed air onto the rotating screens, in particular through nozzles located on either side of the screening mechanism, as indicated in Figure 2(f), or by being located on either side of the screening mechanism Ultrasonic waves generated by the generator are projected onto the rotating screens.
-抽吸藉著該壓縮空氣所揚起之灰塵。- Pumping dust raised by the compressed air.
-將該裝置放置於其最初之位置。- Place the device in its original position.
藉由該壓縮空氣所揚起之灰塵能因此藉著一真空壓力系統(圖1中之8)所吸起,該真空壓力系統係在所有工業粉末製造場所中發現。The dust raised by the compressed air can thus be sucked up by a vacuum pressure system (8 in Fig. 1) which is found in all industrial powder manufacturing sites.
如果這不是該實際情況,該系統可輕易地裝配有一獨立之真空壓力系統。If this is not the case, the system can be easily equipped with a separate vacuum pressure system.
篩網之數目、在每一篩網上藉由該等微粒所花費之時間、及最初導入該篩選機構的微粒之總質量係所有參數,該等熟諳此技藝者將能夠改造他所想要記述特徵之產品的本質。The number of screens, the time spent on the screens by the particles, and the total mass of the particles initially introduced into the screening mechanism are all parameters that are familiar to the artist and will be able to modify what he wants to describe. The essence of the product of the feature.
除了該等微粒之分佈為其粒度測量的一函數以外,本發明允許於一簡化循環期間僅只使用該最大篩孔之篩網,與釋放該最粗糙的微粒之位置,已分析粉末藉著過大直徑微粒之一可能的污染之認知,該污染不可以存在於該粉末中。這些過大直徑之微粒大致上係小量地存在;因此需要使用一簡化之循環,而於一完整循環期間所分析之樣本的質量相比較,能夠採用一高質量之樣本。In addition to the distribution of such particles as a function of their particle size measurement, the present invention allows for the use of only the screen of the largest mesh during a simplified cycle, and the location of the coarsest particles, the analyzed powder by the oversized diameter The perception of possible contamination of one of the particles, which contamination may not be present in the powder. These oversized diameter particles are present substantially in small amounts; therefore, a simplified cycle is required, and a high quality sample can be used as compared to the quality of the samples analyzed during a complete cycle.
因此,本發明之第一目的係一用於記述粉末之粒度測量的特徵之裝置,並設有一進給機構、一排空機構、一稱重機構、一連續震動機構、一篩選機構、及一可能有之控制機構,且其特徵為:-其中該篩選機構係一繞著水平軸心轉動之機構,具有用於一未被佔用的空間或一用於粉末之釋放及導入的空間之至少1位置、用於一抗衝擊板件之1位置、用於不同篩孔之2篩網的至少2位置;-及其中該裝置具有一清潔機構,該清潔機構由至少一噴嘴及/或一位在該篩選機構的周邊上之超音波發生器所組成;-及其中該裝置具有一彈性耦接機構,其位在該篩選機構的水平軸心與該連續震動機構之間。Therefore, the first object of the present invention is a device for describing characteristics of particle size measurement of a powder, and is provided with a feeding mechanism, an emptying mechanism, a weighing mechanism, a continuous vibration mechanism, a screening mechanism, and a There may be a control mechanism, and is characterized in that: - the screening mechanism is a mechanism that rotates about a horizontal axis, and has at least one space for an unoccupied space or a space for release and introduction of powder. Position, at a position of 1 for an impact resistant panel, at least 2 positions for a screen of 2 different screen openings; and wherein the device has a cleaning mechanism consisting of at least one nozzle and/or one An ultrasonic generator on the periphery of the screening mechanism; and wherein the device has an elastic coupling mechanism between the horizontal axis of the screening mechanism and the continuous vibration mechanism.
該進給、排空、稱重、及連續震動機構能以該等熟諳此技藝者早已熟知之所有形式與所有機構製成。The feeding, emptying, weighing, and continuous vibrating mechanisms can be made with all of the mechanisms that are well known to those skilled in the art.
該相同原則應用於該篩選機構,倘若其繞著一水平軸心旋轉,及具有對應於不同篩孔之2篩網的至少4位置、用於該粉末之導入及最粗糙的微粒之釋放的1沒有利用的空間、及1抗衝擊板件。The same principle applies to the screening mechanism, provided that it rotates about a horizontal axis, and has at least 4 positions corresponding to 2 screens of different mesh openings, for the introduction of the powder and the release of the coarsest particles. There is no space to use, and 1 impact resistant panel.
該裝置之特徵亦為其中該抗衝擊板件係由不銹鋼所製成,且係裝配有一使用天然橡膠及聚矽氧膠化體所製成之墊子。The device is also characterized in that the impact resistant member is made of stainless steel and is equipped with a mat made of natural rubber and polyoxygenated gel.
該裝置之特徵亦為其中該彈性耦接機構係以彈性體為基礎的。The device is also characterized in that the resilient coupling mechanism is based on an elastomer.
根據本發明之裝置的特徵亦為其中該篩選機構係在不同形狀中生產,及尤其係圓柱形或多邊形的。The device according to the invention is also characterized in that the screening mechanism is produced in different shapes, and in particular cylindrical or polygonal.
如果可適用,形成本發明之主題的裝置能夠因此包含一控制機構,其功能係控制其他機構。該控制機構可為機械安裝式或偏置式。其可為一電腦、一可程式化之控制器、或該等熟諳此技藝者所早已熟知之任何其他控制機構。If applicable, the device forming the subject matter of the present invention can thus comprise a control mechanism whose function controls other mechanisms. The control mechanism can be mechanically mounted or offset. It can be a computer, a programmable controller, or any other control mechanism that is well known to those skilled in the art.
本發明之另一目的係使用該先前所述裝置,以決定粉末之粒度測量。Another object of the invention is to use the previously described apparatus to determine the particle size measurement of the powder.
根據本發明的裝置之使用的特徵亦為其中該裝置能夠藉著不同之連續位置決定粉末之粒度測量,該等位置係藉由該篩選機構環繞著其水平軸心所取得,該篩選機構之最初位置係在該抗衝擊板件定位在該最低點之處。The use of the device according to the invention is also characterized in that the device is capable of determining the particle size measurement of the powder by means of different successive positions which are obtained by the screening mechanism around its horizontal axis, the initial of the screening mechanism The position is at the lowest point where the impact resistant panel is positioned.
此應用之特徵亦為其中該等微粒之粒度測量的決定線上地發生、亦即在該等微粒之製造過程的進展中發生。This application is also characterized in that the determination of the particle size measurement of the particles occurs on-line, that is, in the progress of the manufacturing process of the particles.
此應用之特徵為其中該等粉末係乾燥粉末,亦即其水含量係少於5質量百分比、及較佳地是少於2質量百分比、與極佳地是少於1質量百分比之粉末,如藉著該粉末的乾燥之前及之後的差別稱重操作所決定者。This application is characterized in that the powders are dry powders, i.e., powders having a water content of less than 5 mass percent, and preferably less than 2 mass percent, and most preferably less than 1 mass percent, such as It is determined by the difference weighing operation before and after drying of the powder.
此應用之特徵亦為其中該等粉末具有一粒度測量範圍,使得該等粉末之平均直徑係於0.05及10毫米之間、較佳地是於0.1及5毫米之間、且極佳地是於0.2及2毫米之間。This application is also characterized in that the powders have a particle size measurement range such that the average diameter of the powders is between 0.05 and 10 mm, preferably between 0.1 and 5 mm, and is excellently Between 0.2 and 2 mm.
此應用之特徵亦為其中該等粉末係用於該食物生產領域之粉末,諸如以糖結晶為基礎之粉末、鹽粉、麵粉、奶粉、由脫水食品材料所構成之粉末、洗衣粉、陶瓷粉末、塑膠粉末、金屬粉末、油漆粉末、藥物粉末、用於印刷之碳粉、肥料、或再者由礦物物質所組成之粉末、與甚至更特別地是天然及/或沉澱之以碳酸鈣為基礎及/或以白雲石為基礎及/或以滑石為基礎之礦物物質粉末、且甚至更特別地是具有一以天然碳酸鈣為基礎之礦物物質的粉末,該礦物物質係大理石、白堊、石灰岩、或其混合物。This application is also characterized in that the powders are used in the food production field, such as powders based on sugar crystals, salt powder, flour, milk powder, powders composed of dehydrated food materials, washing powders, ceramic powders. , plastic powder, metal powder, paint powder, pharmaceutical powder, toner for printing, fertilizer, or powder composed of mineral matter, and even more particularly natural and/or precipitated based on calcium carbonate And/or a mineral powder based on dolomite and/or based on talc, and even more particularly a powder having a mineral material based on natural calcium carbonate, which is marble, chalk, limestone, Or a mixture thereof.
以下之範例說明本發明,然而不會限制其範圍。The following examples illustrate the invention but are not intended to limit its scope.
此範例說明本發明對於一粉末之粒度測量的特徵記述之使用,該粉末係藉由該OMYATM 公司於其薩勒斯(法國)製造廠中所製成,且隨後在DurcalTM 130的名稱之下銷售的碳酸鈣。This example illustrates the use of the present invention is described for a powder of a particle size measured characteristic, the powder based thereon by the company OMYA TM Salles (France) made in the factory, and then the name of Durcal TM 130 Calcium carbonate sold under.
為完成此,根據本發明之裝置係裝配有4個篩網,其篩孔係等於100微米、250微米、355微米及500微米,滿足上述粉末之分析要求(顧客品質規格等)。在用於該等最粗糙的微粒之釋放的位置,在每一篩網上藉由該粉末所花費之時間分別係等於06:00分鐘、07:30分鐘、04:00分鐘、00:30分鐘、及最後00:25分鐘。To accomplish this, the apparatus according to the present invention is equipped with four screens having a mesh size equal to 100 micrometers, 250 micrometers, 355 micrometers, and 500 micrometers, satisfying the analytical requirements of the above powder (customer quality specifications, etc.). At the location for the release of the coarsest particles, the time spent on the screen by the powder is equal to 06:00 minutes, 07:30 minutes, 04:00 minutes, 00:30 minutes, respectively. And the last 00:25 minutes.
在表1中指示該等對應之結果,其表示為微粒的一百分比,該等微粒之直徑係大於每一篩網之篩孔(稱為一項拒絕)。The results of these correspondences are indicated in Table 1, which is expressed as a percentage of the particles, the diameter of which is greater than the size of each screen (referred to as a rejection).
因此表1示範其係可能使用根據本發明之裝置獲得諸如碳酸鈣的粉末之粒度測量分佈。Thus Table 1 demonstrates that it is possible to obtain a particle size measurement distribution of a powder such as calcium carbonate using the apparatus according to the invention.
此範例之目的係藉著說明在該等相同樣本上用該裝置所作成之測量及於該實驗室中手動地作成的測量間之相互關係,以示範根據本發明的裝置之可靠性。The purpose of this example is to demonstrate the reliability of the apparatus according to the present invention by illustrating the correlation between the measurements made with the apparatus on the same sample and the measurements made manually in the laboratory.
此範例使用一粉末,該粉末係藉由該OMYATM 公司於其薩勒斯(法國)製造廠中所製成,且隨後在DurcalTM 130的名稱之下銷售的碳酸鈣。This example uses a powder, the powder-based thereon by the company OMYA TM Salles (France) made in the factory, and then marketed under the name of Durcal TM 130 calcium carbonate.
該粉末之不同樣本係藉著在與範例1所敘述者相同之條件下,根據本發明之裝置所分析。The different samples of the powder were analyzed according to the apparatus of the present invention under the same conditions as those described in Example 1.
同時,這些樣本經過一100微米篩網、及另一250微米篩網被手動地篩選。At the same time, the samples were manually screened through a 100 micron screen and another 250 micron screen.
在此文件之尾端,圖3及圖4分別代表根據該實驗室手動測試之測量拒絕值(縱座標軸、或y軸),如一根據本發明所測量之拒絕值(橫座標軸、或x軸)的一函數:-在100微米(表示在圖3,在此方程式之線性迴歸的直線係y=1.0018x,且其迴歸係數等於0.9751);-在250微米(表示在圖4,在此方程式之線性迴歸的直線係y=1.1437x,且其迴歸係數等於0.9856)。At the end of this document, Figures 3 and 4 respectively represent the measured rejection values (ordinate axis, or y-axis) according to the manual test of the laboratory, such as a rejection value (horizontal axis, or x-axis) measured according to the present invention. A function of: - at 100 microns (shown in Figure 3, the linear regression of the equation is y = 1.018x, and its regression coefficient is equal to 0.9751); - at 250 microns (shown in Figure 4, in this equation The linear regression linear system y = 1.1437x, and its regression coefficient is equal to 0.9856).
圖3及圖4之讀數示範在100微米與250微米手動地作成測量間之優異的相互關係,且那些測量藉由根據本發明之裝置在該等相同之樣本上所直接地獲得(此相互關係自然地係可能用在異於DurcalTM 130之產品、及用於其他粒度測量點,諸如63微米、80微米、355微米等)。The readings of Figures 3 and 4 demonstrate an excellent correlation between the measurements made manually at 100 microns and 250 microns, and those measurements are obtained directly on the same sample by the device according to the invention (this correlation) naturally, different from the system may be used on products Durcal TM 130, the particle size and for other measuring points, such as 63 microns, 80 microns, 355 microns, etc.).
此範例說明本發明對於一粉末之粒度測量的特徵記述之應用,該粉末係呈粉末形式之結晶化的白糖,並藉由該Cristal UnionTM 公司於其Corbeilles(法國)製造廠中所製成,且隨後以糖粉之形式銷售。This example illustrates the application of the present invention is described for the measurement of a particle size characteristics of the powder, the powder of a crystalline powder-based forms of sugar, and by the company Cristal Union TM thereon Corbeilles (France) made in the factory, And then sold in the form of powdered sugar.
為達成此,根據本發明之裝置係裝配有5個篩網,其篩孔係等於125微米、250微米、500微米、630微米、及800微米,滿足上述粉末之分析要求(顧客品質規格等)。在用於該等最粗糙的微粒之釋放的位置,在每一篩網上藉由該粉末所花費之時間分別係等於06:30分鐘、06:00分鐘、06:00分鐘、05:00分鐘、03:30分鐘、及最後02:30分鐘。To achieve this, the apparatus according to the present invention is equipped with five screens having a mesh size equal to 125 micrometers, 250 micrometers, 500 micrometers, 630 micrometers, and 800 micrometers, satisfying the analysis requirements of the above powder (customer quality specifications, etc.) . At the location for the release of the coarsest particles, the time spent on the screen by the powder is equal to 06:30 minutes, 06:00 minutes, 06:00 minutes, 05:00 minutes, respectively. , 03:30 minutes, and finally 02:30 minutes.
在表2中指示該等對應之結果,其表示為微粒的一百分比,該等微粒之直徑係大於每一篩網之篩孔(稱為一項拒絕)。The results of these correspondences are indicated in Table 2, which is expressed as a percentage of the particles, the diameter of which is greater than the mesh of each screen (referred to as a rejection).
因此表2示範其係可能使用根據本發明之裝置獲得諸如糖的粉末之粒度測量分佈。Table 2 therefore demonstrates that it is possible to obtain a particle size measurement distribution of a powder such as sugar using the apparatus according to the invention.
此範例之目的係藉著說明在該等相同樣本上用該裝置所作成之測量及於該實驗室中手動地作成的測量間之相互關係,以示範根據本發明的裝置之可靠性。此範例使用一粉末,該粉末係藉由該Cristal UnionTM 公司於其Corbeilles(法國)製造廠中所製成,且隨後以CandyTM 之名稱所銷售的結晶化糖。The purpose of this example is to demonstrate the reliability of the apparatus according to the present invention by illustrating the correlation between the measurements made with the apparatus on the same sample and the measurements made manually in the laboratory. This example uses a powder, the powder-based company by the Cristal Union TM thereon Corbeilles (France) made in the factory, and then the name Candy TM sold crystallization of sugar.
該等粉末之不同樣本係藉著在與範例3所敘述者相同之條件下,根據本發明之裝置所分析。同時,這些樣本經過一250微米篩網、及另一630微米篩網被手動地篩選。The different samples of the powders were analyzed by the apparatus according to the invention under the same conditions as those described in Example 3. At the same time, the samples were manually screened through a 250 micron screen and another 630 micron screen.
在此文件之尾端,圖5及圖6分別代表根據該實驗室手動測試之測量拒絕值(縱座標軸、或y軸),如一根據本發明所測量之拒絕值(橫座標軸、或x軸)的一函數:-在250微米(表示在圖5,在此方程式之線性迴歸的直線係y=1.0175x-1.51,且其迴歸係數等於0.986);-在630微米(表示在圖6,在此方程式之線性迴歸的直線係y=0.9773x-0.6,且其迴歸係數等於0.988)。At the end of this document, Figures 5 and 6 respectively represent the measured rejection values (ordinate axis, or y-axis) according to the manual test of the laboratory, such as a rejection value (horizontal axis, or x-axis) measured according to the present invention. A function of: - at 250 microns (shown in Figure 5, the linear regression of the equation in this equation is y = 1.0175x-1.51, and its regression coefficient is equal to 0.986); - at 630 microns (shown in Figure 6, here) The linear regression of the equation is y = 0.9773x-0.6 and its regression coefficient is equal to 0.988).
圖5及圖6之讀數示範在250微米與630微米手動地作成測量間之優異的相互關係,且那些測量藉由根據本發明之裝置在該等相同之樣本上所直接地獲得(此相互關係自然地係可能用在不同型式之結晶化糖、及用於其他粒度測量點,諸如125微米、500微米、800微米等)。The readings of Figures 5 and 6 demonstrate an excellent correlation between the measurements made manually at 250 microns and 630 microns, and those measurements are obtained directly on the same sample by the device according to the invention (this correlation) Naturally, it may be used in different types of crystallized sugars, and for other particle size measurement points, such as 125 microns, 500 microns, 800 microns, etc.).
1...進給機構1. . . Feeding mechanism
2...篩選機構2. . . Screening agency
3...水平軸心3. . . Horizontal axis
4...連續震動機構4. . . Continuous vibration mechanism
5...彈性耦接機構5. . . Elastic coupling mechanism
6...排空機構6. . . Emptying mechanism
7...稱重機構7. . . Weighing mechanism
8...真空壓力系統8. . . Vacuum pressure system
a...抗衝擊板件a. . . Impact resistant plate
b...篩網b. . . Screen
c...篩網c. . . Screen
d...篩網d. . . Screen
e...開口e. . . Opening
圖1代表形成本發明之主題的裝置之極概要的面朝上視圖;該畫有陰影線的部份代表該機架,形成本發明之主題的裝置係緊繫至該機架上,以便在該裝置的不同機構之間形成一接合。BRIEF DESCRIPTION OF THE DRAWINGS Figure 1 is a schematic top plan view of a device forming the subject of the present invention; the hatched portion represents the frame, and the device forming the subject of the present invention is fastened to the frame for A joint is formed between the different mechanisms of the device.
圖2示意地顯示圓柱形篩選機構。Figure 2 shows schematically a cylindrical screening mechanism.
圖3顯示根據本發明所測量之拒絕值。Figure 3 shows the rejection values measured in accordance with the present invention.
圖4顯示根據本發明所測量之拒絕值。Figure 4 shows the rejection values measured in accordance with the present invention.
圖5顯示根據本發明所測量之拒絕值。Figure 5 shows the rejection values measured in accordance with the present invention.
圖6顯示根據本發明所測量之拒絕值。Figure 6 shows the rejection values measured in accordance with the present invention.
1...進給機構1. . . Feeding mechanism
2...篩選機構2. . . Screening agency
3...水平軸心3. . . Horizontal axis
4...連續震動機構4. . . Continuous vibration mechanism
5...彈性耦接機構5. . . Elastic coupling mechanism
6...排空機構6. . . Emptying mechanism
7...稱重機構7. . . Weighing mechanism
8...真空壓力系統8. . . Vacuum pressure system
Claims (19)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0608038A FR2906031B1 (en) | 2006-09-14 | 2006-09-14 | DEVICE FOR CHARACTERIZING GRANULOMETRY OF POWDERS AND USES THEREOF. |
Publications (2)
Publication Number | Publication Date |
---|---|
TW200821053A TW200821053A (en) | 2008-05-16 |
TWI441691B true TWI441691B (en) | 2014-06-21 |
Family
ID=37686042
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW096133694A TWI441691B (en) | 2006-09-14 | 2007-09-10 | Device for characterisation of the granulometry of powders and its uses |
Country Status (15)
Country | Link |
---|---|
US (1) | US8123040B2 (en) |
EP (1) | EP2069754B1 (en) |
JP (1) | JP5261800B2 (en) |
KR (1) | KR101449074B1 (en) |
CN (1) | CN101529225B (en) |
AU (1) | AU2007297242B2 (en) |
BR (1) | BRPI0716736B1 (en) |
CA (1) | CA2663195C (en) |
EA (1) | EA013719B1 (en) |
EG (1) | EG25372A (en) |
ES (1) | ES2661029T3 (en) |
FR (1) | FR2906031B1 (en) |
MX (1) | MX2009002630A (en) |
TW (1) | TWI441691B (en) |
WO (1) | WO2008032192A2 (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2906031B1 (en) * | 2006-09-14 | 2009-01-30 | Omya S A S Soc Par Actions Sim | DEVICE FOR CHARACTERIZING GRANULOMETRY OF POWDERS AND USES THEREOF. |
KR101419174B1 (en) * | 2013-04-18 | 2014-07-14 | 창원대학교 산학협력단 | Outdoor particle size distribution analyzer |
EP3138417A1 (en) * | 2013-11-26 | 2017-03-08 | Electrolux Professional S.p.A. | Foodstuff sieve station |
CN108507911B (en) * | 2018-04-24 | 2024-07-16 | 佛山市汇创科技有限公司 | Multifunctional powder detection equipment |
CN109092661B (en) * | 2018-08-10 | 2021-09-21 | 孙江花 | Screen drum formula screening sand device for building |
CN113702253A (en) * | 2021-07-08 | 2021-11-26 | 中国科学院金属研究所 | Method for detecting particle size of ultrafine powder for selective laser melting forming |
JP2023105977A (en) * | 2022-01-20 | 2023-08-01 | トヨタ自動車株式会社 | Electrode manufacturing method, classification system, electrode material, and electrode |
CN114800943B (en) * | 2022-05-20 | 2024-02-20 | 嘉兴学院 | Method for recycling waste carpets |
CN117531697B (en) * | 2023-11-14 | 2024-04-19 | 广东工业大学 | Semi-automatic vibrating screen device for silt |
Family Cites Families (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2537159A (en) * | 1946-04-15 | 1951-01-09 | Sallander Court Gosta Valdemar | Vibrator |
AT267988B (en) * | 1967-03-10 | 1969-01-27 | Losenhausen Maschinenbau Ag | Vibrating roller |
US3749372A (en) * | 1972-01-27 | 1973-07-31 | Funk Mfg Co | Yieldable support means and drive mechanism for concrete mixer drums |
CH604932A5 (en) * | 1974-06-12 | 1978-09-15 | Karlsruhe Augsburg Iweka | |
FR2349369A2 (en) * | 1976-04-27 | 1977-11-25 | Tytko Jean | ROTARY SIEVING APPARATUS, ADAPTABLE TO DIFFERENT ROTATING MEANS, INCLUDING CONCRETE MIXING MACHINES |
US4135388A (en) | 1977-10-31 | 1979-01-23 | Georgia Tech Research Institute | Method and apparatus for automatically fractionating a sample of particulate material into discrete size fractions |
US4282090A (en) * | 1980-06-20 | 1981-08-04 | St. Louis Conveyor Company Inc. | Rotary sifting device |
JPS5982584U (en) * | 1982-11-22 | 1984-06-04 | 川本工業株式会社 | Rubber liner mounting structure |
US4487323A (en) * | 1983-05-09 | 1984-12-11 | Weyerhaeuser Company | Automatic particle-size analyzer |
JPS60176280U (en) * | 1984-04-27 | 1985-11-21 | 川崎重工業株式会社 | vibrating sieve device |
JPS61216779A (en) * | 1985-03-23 | 1986-09-26 | 金子農機株式会社 | Unhulled rice selector |
JPH067827Y2 (en) * | 1989-03-14 | 1994-03-02 | 三菱原子燃料株式会社 | Powder conditioner |
JPH0975758A (en) * | 1995-09-12 | 1997-03-25 | Rasa Ind Ltd | Conical crusher |
GB2356711B (en) * | 1999-11-25 | 2003-01-22 | Technometrics Ltd | Particle size distribution analyser |
CN2428227Y (en) * | 2000-04-20 | 2001-05-02 | 高焰 | Tube like multifunction vibration sieve |
CN2497889Y (en) * | 2001-09-25 | 2002-07-03 | 李文跃 | Centrifugal airstream powder screener |
KR100533173B1 (en) * | 2003-05-07 | 2005-12-01 | (주)디테코 | A apparatus to sort materials |
FR2886014B1 (en) * | 2005-05-17 | 2007-08-10 | Omya S A S Soc Par Actions Sim | DEVICE FOR CHARACTERIZING POWDER GRANULOMETRY AND USES THEREOF. |
FR2906031B1 (en) * | 2006-09-14 | 2009-01-30 | Omya S A S Soc Par Actions Sim | DEVICE FOR CHARACTERIZING GRANULOMETRY OF POWDERS AND USES THEREOF. |
-
2006
- 2006-09-14 FR FR0608038A patent/FR2906031B1/en active Active
-
2007
- 2007-09-10 TW TW096133694A patent/TWI441691B/en not_active IP Right Cessation
- 2007-09-12 CA CA2663195A patent/CA2663195C/en not_active Expired - Fee Related
- 2007-09-12 CN CN2007800392701A patent/CN101529225B/en not_active Expired - Fee Related
- 2007-09-12 AU AU2007297242A patent/AU2007297242B2/en not_active Ceased
- 2007-09-12 EP EP07825104.8A patent/EP2069754B1/en active Active
- 2007-09-12 JP JP2009527915A patent/JP5261800B2/en not_active Expired - Fee Related
- 2007-09-12 KR KR1020097006914A patent/KR101449074B1/en active IP Right Grant
- 2007-09-12 MX MX2009002630A patent/MX2009002630A/en active IP Right Grant
- 2007-09-12 US US12/310,741 patent/US8123040B2/en active Active
- 2007-09-12 EA EA200970277A patent/EA013719B1/en not_active IP Right Cessation
- 2007-09-12 ES ES07825104.8T patent/ES2661029T3/en active Active
- 2007-09-12 WO PCT/IB2007/002644 patent/WO2008032192A2/en active Application Filing
- 2007-09-12 BR BRPI0716736-9A patent/BRPI0716736B1/en not_active IP Right Cessation
-
2009
- 2009-03-11 EG EG2009030321A patent/EG25372A/en active
Also Published As
Publication number | Publication date |
---|---|
WO2008032192A3 (en) | 2008-05-22 |
KR101449074B1 (en) | 2014-10-08 |
CN101529225B (en) | 2013-04-17 |
JP2010503849A (en) | 2010-02-04 |
ES2661029T3 (en) | 2018-03-27 |
BRPI0716736B1 (en) | 2018-08-14 |
EP2069754B1 (en) | 2017-11-29 |
TW200821053A (en) | 2008-05-16 |
CA2663195A1 (en) | 2008-03-20 |
EP2069754A2 (en) | 2009-06-17 |
AU2007297242A1 (en) | 2008-03-20 |
JP5261800B2 (en) | 2013-08-14 |
CA2663195C (en) | 2014-07-08 |
WO2008032192A2 (en) | 2008-03-20 |
FR2906031B1 (en) | 2009-01-30 |
EG25372A (en) | 2011-12-20 |
US20090281654A1 (en) | 2009-11-12 |
US8123040B2 (en) | 2012-02-28 |
FR2906031A1 (en) | 2008-03-21 |
AU2007297242B2 (en) | 2011-09-15 |
EA200970277A1 (en) | 2009-10-30 |
KR20090068228A (en) | 2009-06-25 |
EA013719B1 (en) | 2010-06-30 |
MX2009002630A (en) | 2009-03-24 |
BRPI0716736A2 (en) | 2013-09-17 |
CN101529225A (en) | 2009-09-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TWI441691B (en) | Device for characterisation of the granulometry of powders and its uses | |
Dapkunas et al. | Particle size characterization | |
US20170284928A1 (en) | Processing of solid micron sized particles for rapid deposition on substrate surfaces with uniform particle distribution | |
Šupuk et al. | Tribo-electrification and associated segregation of pharmaceutical bulk powders | |
Pieper et al. | Numerical modeling of an automated optical belt sorter using the Discrete Element Method | |
JP5740852B2 (en) | Powder cutting device and powder foreign matter inspection device using the same | |
JP2012007999A (en) | Particulate foreign material inspecting device using particulate sieving device | |
Ku | Evaluation of the behavior of ceramic powders under mechanical vibration and its effect on the mechanics of auto-granulation | |
JPS5851964A (en) | Screen apparatus | |
Daleffe et al. | Analysis of the effect of particle size distributions on the fluid dynamic behavior and segregation patterns of fluidized, vibrated and vibrofluidized beds | |
Patil | Mechanical Operations | |
Dupas et al. | Experimental study on the impact of key material properties on flowability of sucrose and maltodextrin | |
WO2006123037A1 (en) | Device for determining powder particle size distribution and uses thereof | |
Merkus et al. | Sieves and sieving | |
JP2009008644A (en) | Method for evaluating dispersibility of powder, method for evaluating concentration of airborne powder, and method for designing containment facility of powder using the same | |
Bernhardt et al. | Sieving | |
Londershausen et al. | Characterization of powder layer dustiness–influence of the deposit thickness | |
Daeschner et al. | Application of electroformed precision micromesh sieves to the determination of particle size distribution | |
Yao | Evaluating the physical and insecticidal properties and the effects on grain flow properties of a synthetic amorphous zeolite intended for grain protection | |
Langeteig | Development of an inexpensive test-rig for particle sensors | |
Figura et al. | Geometric Properties: Size and Shape | |
Sultanbawa | Kinetic Studies of Particle Separation by Sievin | |
Salihu | Design and optimisation of a spring particle sizer | |
Elskamp | A framework for the derivation of dynamic process models for sieving | |
Bokelman et al. | Evaluating the Accuracy of the 3-Sieve Particle Size Analysis Method Compared to the 12-Sieve Method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
MM4A | Annulment or lapse of patent due to non-payment of fees |